JPH08168633A - Use of filter for gasket-free/frame-free odor emitting substance and/or harmful substance - Google Patents
Use of filter for gasket-free/frame-free odor emitting substance and/or harmful substanceInfo
- Publication number
- JPH08168633A JPH08168633A JP7174368A JP17436895A JPH08168633A JP H08168633 A JPH08168633 A JP H08168633A JP 7174368 A JP7174368 A JP 7174368A JP 17436895 A JP17436895 A JP 17436895A JP H08168633 A JPH08168633 A JP H08168633A
- Authority
- JP
- Japan
- Prior art keywords
- use according
- adsorbent
- filter layer
- adsorption filter
- adhesive
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000126 substance Substances 0.000 title claims abstract description 17
- 239000003463 adsorbent Substances 0.000 claims abstract description 30
- 239000000853 adhesive Substances 0.000 claims abstract description 22
- 230000001070 adhesive effect Effects 0.000 claims abstract description 22
- 238000012856 packing Methods 0.000 claims abstract description 12
- 239000012876 carrier material Substances 0.000 claims abstract description 9
- 238000004378 air conditioning Methods 0.000 claims abstract description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 39
- 238000001179 sorption measurement Methods 0.000 claims description 32
- 239000002245 particle Substances 0.000 claims description 19
- 229920005830 Polyurethane Foam Polymers 0.000 claims description 12
- 239000011496 polyurethane foam Substances 0.000 claims description 12
- 229920001577 copolymer Polymers 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 9
- 239000006260 foam Substances 0.000 claims description 6
- 239000011148 porous material Substances 0.000 claims description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 125000005442 diisocyanate group Chemical group 0.000 claims description 4
- 239000002808 molecular sieve Substances 0.000 claims description 4
- 229920001228 polyisocyanate Polymers 0.000 claims description 4
- 239000005056 polyisocyanate Substances 0.000 claims description 4
- 239000004814 polyurethane Chemical class 0.000 claims description 4
- 230000003014 reinforcing effect Effects 0.000 claims description 4
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 4
- 230000002209 hydrophobic effect Effects 0.000 claims description 3
- 229920002635 polyurethane Chemical class 0.000 claims description 3
- 239000004925 Acrylic resin Substances 0.000 claims description 2
- 238000004438 BET method Methods 0.000 claims description 2
- 239000004793 Polystyrene Substances 0.000 claims description 2
- 150000001242 acetic acid derivatives Chemical class 0.000 claims description 2
- 150000001252 acrylic acid derivatives Chemical class 0.000 claims description 2
- 230000003213 activating effect Effects 0.000 claims description 2
- 125000003277 amino group Chemical group 0.000 claims description 2
- 239000003957 anion exchange resin Substances 0.000 claims description 2
- 238000010000 carbonizing Methods 0.000 claims description 2
- 230000006835 compression Effects 0.000 claims description 2
- 238000007906 compression Methods 0.000 claims description 2
- 150000004985 diamines Chemical class 0.000 claims description 2
- 230000000873 masking effect Effects 0.000 claims description 2
- 229920000620 organic polymer Polymers 0.000 claims description 2
- 229920000768 polyamine Polymers 0.000 claims description 2
- 229920002223 polystyrene Polymers 0.000 claims description 2
- 229920005990 polystyrene resin Polymers 0.000 claims description 2
- 229920002689 polyvinyl acetate Polymers 0.000 claims description 2
- 239000011118 polyvinyl acetate Substances 0.000 claims description 2
- 239000003729 cation exchange resin Substances 0.000 claims 1
- 239000000383 hazardous chemical Substances 0.000 claims 1
- 239000000463 material Substances 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000003456 ion exchange resin Substances 0.000 description 3
- 229920003303 ion-exchange polymer Polymers 0.000 description 3
- 229920002126 Acrylic acid copolymer Polymers 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000002787 reinforcement Effects 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011294 coal tar pitch Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28042—Shaped bodies; Monolithic structures
- B01J20/28045—Honeycomb or cellular structures; Solid foams or sponges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1669—Cellular material
- B01D39/1676—Cellular material of synthetic origin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28011—Other properties, e.g. density, crush strength
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
- B01J20/28019—Spherical, ellipsoidal or cylindrical
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28069—Pore volume, e.g. total pore volume, mesopore volume, micropore volume
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28095—Shape or type of pores, voids, channels, ducts
- B01J20/28097—Shape or type of pores, voids, channels, ducts being coated, filled or plugged with specific compounds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S55/00—Gas separation
- Y10S55/42—Foam filter materials
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Separation Of Gases By Adsorption (AREA)
- Filtering Materials (AREA)
- Air-Conditioning For Vehicles (AREA)
- Air Filters, Heat-Exchange Apparatuses, And Housings Of Air-Conditioning Units (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、空気供給チヤンネル
(例えば、空調設備、自動車または交通手段)における
臭気発生物質および/または有害物質フイルタとしての
吸着フイルタ層の使用に関する。FIELD OF THE INVENTION The present invention relates to the use of adsorbent filter layers as odor generating and / or toxic filter in air supply channels (eg air conditioning, motor vehicles or transportation).
【0002】[0002]
【従来の技術】従来の粒子フイルタは、現在の知見によ
れば、空気流(例えば、空調設備の空気流、自動車の供
給空気、etc. )の浄化には不十分である。なぜなら
ば、上記フイルタは、過去において健康に対する作用が
軽視されていたガス状成分(特に、臭気発生物質または
有害物質)を抑止するのに不十分である。従って、粒子
フイルタの後ろに吸着フイルタを配置した。2. Description of the Related Art Conventional particle filters are, according to current knowledge, insufficient for cleaning air streams (for example, air streams for air-conditioning equipment, air supply for motor vehicles, etc.). This is because the filter is insufficient to suppress gaseous components (especially odor-producing substances or harmful substances) whose effects on health have been neglected in the past. Therefore, the adsorption filter was placed after the particle filter.
【0003】現在、吸着フイルタは、主として、活性炭
をベースとして製造される。定置の設備には、概ね、薄
い粒子層が使用されるが、これは、自動車の分野には不
適である。しかしながら、粒子層フイルタは、常に、粒
径に関して妥協する必要がある。即ち、動力学的には、
小さい吸着剤粒子が要求され、一方、圧力降下を減少す
るという目的に関しては、粒子を大きくしなければなら
ない。この場合、更に、通路形成が容易でなければなら
ない。保守または交換が困難であり、汚染が増大する。
“膨張固定床”原理の開発によつて、上記欠点の大半は
除かれた。この原理の場合、概ねプレート状の開放した
担体構造体に小さい吸着剤粒子を固定する。かくして、
粒径に関する妥協が避けられる。更に、ダストを含まな
いプレート状フイルタ要素を容易に交換でき、従って、
保守作業が、従来のフイルタの場合よりも本質的に楽に
なる。At present, adsorption filters are mainly manufactured on the basis of activated carbon. Stationary installations generally use thin particle layers, which is unsuitable for the automotive field. However, particle layer filters always have to compromise on particle size. That is, dynamically,
Small adsorbent particles are required, while for the purpose of reducing pressure drop the particles must be large. In this case, the passage should also be easy to form. Difficult to maintain or replace and increase pollution.
With the development of the "expanded fixed bed" principle, most of the above drawbacks have been eliminated. In the case of this principle, small adsorbent particles are fixed to a generally plate-shaped open carrier structure. Thus,
A compromise on particle size is avoided. Furthermore, the dust-free plate-shaped filter element can be easily replaced, thus
Maintenance work is inherently easier than with traditional filters.
【0004】自動車室内の空気供給チヤンネルに関して
は、プレートフイルタまたは折畳フイルタが導入されて
いるか、開発されつつある。プレートフイルタは、“膨
張固定床”の原理にもとづき、相互に接着された活性炭
粒子から構成できる。上記フイルタ媒体をフレームにパ
ツキンによつて固定するか、発泡充填させ、上記フレー
ムを空気供給チヤンネルに組込む。上記フイルタの本質
的欠点は、フレームおよびパツキンにもとづきフイルタ
の占有スペースが大きく、その製造が煩瑣であり、従っ
て、製造コストが高く、相互に強固に結合された各種材
料が物質分離を妨害するので、上記フイルタの廃棄また
はリサイクルの場合、大きな問題が生ずるという点にあ
る。For air supply channels in the passenger compartment, plate or folding filters have been introduced or are being developed. The plate filter can be composed of activated carbon particles adhered to each other based on the principle of "expanded fixed bed". The filter medium is fixed to the frame with a packing or foam-filled, and the frame is incorporated into the air supply channel. The essential drawback of the above filter is that the filter occupies a large space on the basis of the frame and the packing, and its manufacturing is complicated, so that the manufacturing cost is high and various materials firmly bonded to each other interfere with the substance separation. In the case of discarding or recycling the above filter, a big problem occurs.
【0005】[0005]
【発明が解決しようとする課題】本発明の課題は、パツ
キンおよびフレームを含まない臭気発生物質または有害
物質フイルタを製造することにある。SUMMARY OF THE INVENTION An object of the present invention is to produce an odor generating substance or harmful substance filter which does not include a packing and a frame.
【0006】[0006]
【課題を解決するための手段】この課題は、本発明にも
とづき、接着剤によつて吸着剤を固定した高通気性担体
材料からなり僅かに圧縮して空気供給チヤンネルに導入
した自立の弾性吸着フイルタ層を無パツキン・無フレー
ム形臭気発生物質および/または有害物質フイルタとし
て使用することによつて、解決される。この吸着フイル
タ層は、“膨張固定床”原理にもとづくフイルタ媒体で
ある。This object is based on the invention on the basis of the invention of a self-supporting elastic adsorption, which consists of a highly permeable carrier material with an adsorbent fixed by an adhesive and is slightly compressed and introduced into an air supply channel. It is solved by using the filter layer as a packing-free frameless odor generating substance and / or harmful substance filter. This adsorption filter layer is a filter medium based on the "expanded fixed bed" principle.
【0007】自立の弾性吸着フイルタ層は公知である。
即ち、DE−A−3813563には、活性炭を装填し
た網状ポリウレタンフオームからなるフイルタ材料が記
載されている。Self-supporting elastic adsorption filter layers are known.
That is, DE-A-3815563 describes a filter material consisting of reticulated polyurethane foam loaded with activated carbon.
【0008】本発明の特殊な実施例の場合、この種の吸
着フイルタ層を空調設備、自動車または交通手段に使用
する。高通気性担体材料としては、気孔の大きいすべて
のフオーム(特に、網状ポリウレタンフオーム)を使用
できる。In a special embodiment of the invention, an adsorption filter layer of this kind is used for air conditioning, motor vehicles or transportation. As the highly permeable carrier material, all foams having large pores (in particular, reticulated polyurethane foam) can be used.
【0009】この場合、上記担体材料のスケルトンに、
接着剤によつて吸着剤を固定できる。かくして、自立の
吸着フイルタ層が生ずる。本発明にもとづき使用する吸
着フイルタ層については、既に、廃棄方法またはリサイ
クル方法が存在する。In this case, in the skeleton of the carrier material,
The adsorbent can be fixed by an adhesive. Thus, a self-supporting adsorption filter layer results. With respect to the adsorption filter layer used according to the present invention, there is already a disposal method or a recycling method.
【0010】吸着フイルタ層は、本発明に係る使用のた
めに、十分な弾性および十分に高い形状安定性を有して
いなければならない。吸着剤フイルタ層が、載置面エツ
ジ(例えば、テーブルエツジ)から20cmだけ突出
し、上記エツジの最外側端が、吸着フイルタ層の厚さの
2〜10倍(特に、2〜5倍)だけ下降する場合、吸着
フイルタ層の十分な弾性および十分に高い形状安定性が
得られる。この場合、より厚いプレートは、薄いプレー
トよりも、明らかに垂下度が小さい。The adsorption filter layer must have sufficient elasticity and sufficiently high dimensional stability for use according to the present invention. The adsorbent filter layer projects by 20 cm from the mounting surface edge (for example, a table edge), and the outermost end of the edge is lowered by 2 to 10 times (particularly 2 to 5 times) the thickness of the adsorption filter layer. In that case, sufficient elasticity and sufficiently high shape stability of the adsorption filter layer can be obtained. In this case, the thicker plate has significantly less droop than the thin plate.
【0011】本発明に係る材料を使用した場合の利点
は、特殊なパツキンおよび補助フオームを使用せずに上
記材料を空気チヤンネルに直接に挿入できるという点に
ある。挿入を容易化するため、もちろん、空気チヤンネ
ルに細い案内レールを設けることができる。The advantage of using the material according to the invention is that it can be inserted directly into the air channel without the use of special packings and auxiliary foams. To facilitate insertion, of course, the air channel can be provided with a thin guide rail.
【0012】開放気孔の網状ポリウレタンフオームは、
8〜30ppi(1インチ当りの気孔数)を有すること
ができる。このようなフオームは、例えば、EP−B−
340542に記載されている。The open-pore reticulated polyurethane foam is
It can have 8-30 ppi (pores per inch). Such a form is, for example, EP-B-
340542.
【0013】上記ポリウレタンフオームに接着剤を塗布
し、次いで、粒径0.3〜1mmの適切な吸着剤を装填
する。フオームの内表面のこの装填(特に、完全な装
填)によつて、極めて高い剛性が得られる。しかしなが
ら、材料は、なお、十分に圧縮でき、従って、対応する
過大寸法のプレートをこのために設けた空気供給チヤン
ネル内に応力を加えて導入できる。驚くべきことには、
吸着フイルタ層の本発明に係るこの使用によつて、縁範
囲のリーク(いわゆる“縁の通過性”)を完全に回避で
きるということが判つた。An adhesive is applied to the polyurethane foam and then loaded with a suitable adsorbent having a particle size of 0.3 to 1 mm. This loading of the inner surface of the form (in particular full loading) results in a very high rigidity. However, the material is still sufficiently compressible that stressed introduction into the air-supply channel for which corresponding oversized plates are provided for this purpose. Surprisingly,
It has been found that with this use of the adsorption filter layer according to the invention, edge-area leakage (so-called "edge passage") can be avoided altogether.
【0014】本発明の特殊な実施例にもとづき、吸着剤
の粒径は、少なくとも、ポリウレタンフイルタの粒径の
3倍よりも小さい。装填ずみのポリウレタンフオームの
圧縮度は、1〜10N/cm3 の圧力下で、少なくとも
2%でなければならない。According to a special embodiment of the invention, the particle size of the adsorbent is at least smaller than 3 times the particle size of the polyurethane filter. The compressibility of the loaded polyurethane foam should be at least 2% under a pressure of 1-10 N / cm 3 .
【0015】しかしながら、この吸着フイルタ層は、複
数の吸着フイルタ層から構成することもできる。各吸着
フイルタ層の厚さは、一般に、5〜40mm(特に、1
0〜30mm)である。多層吸着フイルタ層の場合、各
層の厚さは約5〜30mmである。However, the adsorption filter layer can be composed of a plurality of adsorption filter layers. The thickness of each adsorption filter layer is generally 5-40 mm (especially 1
0 to 30 mm). In the case of a multilayer adsorption filter layer, the thickness of each layer is about 5-30 mm.
【0016】吸着剤としては下記を使用できる: ・ 活性炭(植物質素材(木材、ビート、石炭、et
c. )を炭化し、次いで、活性化した材料);The following can be used as adsorbents: Activated carbon (plant material (wood, beet, coal, et
c.) carbonized and then activated material);
【0017】・ 0.2〜2mm(好ましくは、0.3
〜1mm)の径、少なくとも900m2 /gの内 表面
積(BET法で測定)および少なくとも10N(好まし
くは、少なくとも30N)のバースト圧(径0.5mm
の球を使用した場合)を有する、石炭タールピツチまた
は 石油残渣からなる球状活性炭(このような球状活性
炭は、例えば、GB−B−1525420、GB−B−
2012257、GB−A−2025385またはGB
−A−2053176に記載されている);0.2 to 2 mm (preferably 0.3 mm)
˜1 mm), an internal surface area of at least 900 m 2 / g (measured by the BET method) and a burst pressure of at least 10 N (preferably at least 30 N) (diameter 0.5 mm).
Spherical activated carbon consisting of coal tar pitch or petroleum residues (for example, GB-B-1525420, GB-B-
2012257, GB-A-2025385 or GB
-A-2053176);
【0018】・ 0.2〜2mm(好ましくは、0.3
〜1mm)の粒径、少なくとも900m2 /gの 内表
面積を有するカーボン片またはカーボン粒(このような
カーボンは、例えば、H. Kienleら、“Akt
ivkohle und ihre industri
elle Anwendung”、Ferdinand
社刊(1980)に記載されている)・スルホン化スチ
レン・ジビニルベンゼン・コポリマーまたはスチレン・
アクリル酸・コポリマーをベースとする、炭化、活性化
せる多孔質ポリマー(この種の炭化ポリマーは、例え
ば、US−A−4040990、US−A−42244
15またはUS−A−4957897に記載されてい
る);0.2-2 mm (preferably 0.3 mm)
Carbon particles or carbon particles having a particle size of ˜1 mm) and an internal surface area of at least 900 m 2 / g (such carbons are described, for example, by H. Kienle et al., “Akt
ivkohle und ihre industry
elle Anwundung ", Ferdinand
(Published in the company (1980)) Sulfonated styrene divinylbenzene copolymer or styrene
Carbonized, activated porous polymers based on acrylic acid copolymers (carbonized polymers of this type are described, for example, in US-A-4040990, US-A-42244).
15 or US-A-4957897);
【0019】・ スルホン化スチレン・ジビニルベンゼ
ン・コポリマーまたはスチレン・アクリル酸・コポリマ
ーをベースとする炭化、活性化せるイオン交換樹脂(こ
の種のイオン交換樹脂からなる活性炭の製造は、例え
ば、DD−B−063768またはDE−A−4304
026に記載されている)または第3または第4アミノ
基を有するポリスチレン樹脂またはポリアクリル樹脂を
ベースとする炭化、活性化せる陰イオン交換樹脂、特
に、ゲルタイプのイオン交換樹脂(この種のイオン交換
樹脂は、例えば、DE−A−4328219に記載され
ている);An ion exchange resin which is based on a sulfonated styrene / divinylbenzene copolymer or a styrene / acrylic acid copolymer and which can be activated by carbonization (for example, the production of activated carbon composed of this type of ion exchange resin is described in DD-B). -063768 or DE-A-4304
No. 026) or a polystyrene resin or polyacrylic resin having a tertiary or quaternary amino group, which is a carbonizing and activating anion exchange resin, in particular a gel type ion exchange resin (of this kind of ions). Exchange resins are described, for example, in DE-A-4328219);
【0020】・ CH2 ブリツジによつて架橋されたス
チレン・ジビニルベンゼン・コポリマーをベースとする
(非炭化の)多孔質ポリマー(このポリマーは、例え
ば、ダウ・ケミカル社から商品名Sorbathene
(登録商標)として市販されている);A (non-carbonized) porous polymer based on a styrene-divinylbenzene copolymer cross-linked by CH 2 bridges (this polymer is commercially available, for example, from Dow Chemical Company under the trade name Sorbathene)
(Commercially available as (registered trademark));
【0021】・ モレキユラーシーブ(特に、SiO2
/Al2 O3 モジユール>10の疎水性モレキユラーシ
ーブ)からなる成形片(これは、例えば、デグサ社から
商品名DAY−Zeolith(登録商標)として市販
されている)。・ Molecular sieves (especially SiO 2
/ Hydrophobic molecular sieve with Al 2 O 3 module> 10) (commercially available, for example, under the trade name DAY-Zeolith® from Degussa).
【0022】吸着剤は、例えば、DE−A−38135
63にもとづき、ポリウレタンフオームに組込むことが
できる。The adsorbent is, for example, DE-A-38135.
According to No. 63, it can be incorporated into a polyurethane foam.
【0023】本発明に係る好ましい実施例の場合、吸着
フイルタ層は、吸着剤50〜400g/l(好ましく
は、150〜350g/l)を含む。In the preferred embodiment of the present invention, the adsorption filter layer comprises 50 to 400 g / l of adsorbent (preferably 150 to 350 g / l).
【0024】吸着フイルタ層に使用される接着剤の量
は、高通気性担体材料の重量の±50%である。接着剤
としては、架橋可能な有機ポリマー(例えば、アクリル
酸誘導体、ポリウレタン誘導体、ポリスチレン誘導体、
ポリシアネート誘導体、ポリビニルアセテート誘導体ま
たは熔融接着剤)を使用できる。本発明の好ましい実施
例にもとづき、接着剤としては、ジアミンおよび/また
はポリアミンで架橋されるマスクせるジイソシアナート
および/またはポリイソシアナートをベースとし溶剤を
含まないプレポリマー2成分系を使用する。上記接着剤
は、良好な初期接着能を有し、架橋段階中、最適な接着
性を与える顕著な最小粘度を示す。接着剤のこの最小粘
度によつて、担体材料と吸着剤との間の接触面積が最小
となり、従って、担体材料の高い通気性が保持される。
この種の系は、好ましくは、バイエル社から“IMPR
ANIL(登録商標)・High・Solid・PUR
・Reaktivprodukte”なる名称で市販さ
れている系である。The amount of adhesive used in the adsorption filter layer is ± 50% by weight of the highly breathable carrier material. As the adhesive, a crosslinkable organic polymer (for example, acrylic acid derivative, polyurethane derivative, polystyrene derivative,
Polycyanate derivatives, polyvinyl acetate derivatives or melt adhesives) can be used. According to a preferred embodiment of the invention, the adhesives used are solvent-free prepolymer two-component systems based on masking diisocyanates and / or polyisocyanates which are crosslinked with diamines and / or polyamines. The adhesive has a good initial adhesion capacity and exhibits a remarkable minimum viscosity which gives optimum adhesion during the crosslinking stage. This minimum viscosity of the adhesive minimizes the contact area between the carrier material and the adsorbent, and thus keeps the carrier material highly breathable.
A system of this kind is preferably manufactured by Bayer AG under the name "IMPR".
ANIL (registered trademark), High, Solid, PUR
-A system that is commercially available under the name "Reaktivproduct".
【0025】別の好ましい接着剤は、マスクされてない
ジイソシアナートポリマーおよび/またはポリイソシア
ネートからなる。この種の接着剤は、例えば、バイエル
社からLevacast(登録商標)Addukt43
131Nなる名称で市販されている。架橋反応は、吸着
剤中の水分にもとづき開始される。Another preferred adhesive consists of unmasked diisocyanate polymers and / or polyisocyanates. An adhesive of this kind is, for example, from Levacast® Addukt 43 from Bayer.
It is marketed under the name 131N. The cross-linking reaction is initiated based on the water content in the adsorbent.
【0026】本発明にもとづき使用するフイルタ層は、
厚さ、吸着剤または接着剤に関して同一の異なる性質を
有する複数の重畳する吸着フイルタ層から構成すること
もできる。The filter layer used according to the invention is
It may also consist of multiple overlapping adsorption filter layers having the same different properties with respect to thickness, adsorbent or adhesive.
【0027】更に、流入側へ僅かに凸に湾曲した弧を有
するよう弾性吸着フイルタ層を構成することができる。
かくして、一方では、吸着フイルタ層の機械的負荷能を
増大でき、他方では、空気供給チヤンネル(または案内
レール)に沿う空気流によつて吸着フイルタ層を圧縮
し、かくして、密封性を更に向上できる。Furthermore, the elastic adsorption filter layer can be constructed so as to have an arc curved slightly convex toward the inflow side.
Thus, on the one hand, the mechanical load capacity of the adsorption filter layer can be increased and, on the other hand, the adsorption filter layer can be compressed by the air flow along the air supply channel (or guide rail), thus further improving the sealing performance. .
【0028】本発明の別の実施例の場合、吸着フイルタ
層の間にまたは空気供給チヤンネルの出口側に補足の補
強要素を設置する。この補強要素も、同じく、パツキン
およびフレームを有していない。この補強要素には、例
えば、格子(特に、ポリアミド格子)が好適である。In another embodiment of the invention, a supplementary reinforcing element is provided between the adsorption filter layers or at the outlet side of the air supply channel. This reinforcing element likewise has no packing and no frame. A lattice, in particular a polyamide lattice, is suitable for this reinforcing element.
【0029】臭気発生物質または有害物質の除去のため
空気供給チヤンネルに本発明にもとづき吸着フイルタ層
を使用したことによつて、フレームまたはパツキンは不
要であり、従って、一方では、製造コストが節減され、
他方では、本質的に環境を損なうことのない廃棄が可能
となる。更に、この吸着フイルタ層の使用によつてフイ
ルタ媒体を簡単に交換できるという利点が得られる。こ
の場合、空気チヤンネルの上面または任意の触手可能な
箇所に、フイルタ媒体に触手できるよう着脱自在の蓋を
設ければよい。僅かに圧縮して空気チヤンネルに導入し
た媒体は、必要に応じて、取出し、更新できる。同様
に、縁パツキンおよび補助フレームを使用することなく
上述の吸着フイルタ層を建屋の空調設備の排気口に設置
できる。更に、自立の非弾性プレートフイルタは、弾性
パツキンを使用せずに空気チヤンネルに設置することは
不可能である。更に、この種のパツキンを使用しても、
補助フレームを使用せずにフイルタプレートを固定する
のは困難である。By using an adsorbent filter layer according to the invention in the air supply channel for the removal of odor-producing substances or harmful substances, no frame or packing is required, so that on the one hand manufacturing costs are reduced. ,
On the other hand, disposal is possible without essentially damaging the environment. Moreover, the use of this adsorption filter layer has the advantage that the filter medium can be easily replaced. In this case, an attachable / detachable lid may be provided on the upper surface of the air channel or on any touchable portion so that the filter medium can be touched. The medium, which is slightly compressed and introduced into the air channel, can be taken out and renewed if necessary. Similarly, the above-mentioned adsorption filter layer can be installed at the exhaust port of the air conditioning equipment of the building without using the edge packing and the auxiliary frame. Moreover, self-supporting inelastic plate filters cannot be installed on the air channel without the use of elastic packing. Furthermore, even if you use this type of packing,
It is difficult to fix the filter plate without using the auxiliary frame.
【0030】[0030]
【実施例】実施例を参照して、以下に、本発明を説明す
る。EXAMPLES The present invention will be described below with reference to examples.
【0031】実施例 1 12ppi、容積重量30g/lおよび厚さ20mmの
網状ポリウレタンフオームに、100部のImpran
il HS 62および6, 2部のImprafix
HSCの混合物を塗布し、圧縮した。圧縮効果は、10
0%である。次いで、フオームマツトにピツチベースの
球状活性炭を散布し、過剰の活性炭を除去し、160°
において(2min)接着剤を凝結させた。球状活性炭
の径は0.4〜0.6mmであり、内表面積は、110
0m2 /gであり、量は195g/lである。Example 1 100 parts of Impran on 12 ppi, 30 g / l volume weight and 20 mm thick reticulated polyurethane foam.
il HS 62 and 6, 2 parts Imprafix
A mixture of HSC was applied and compressed. The compression effect is 10
It is 0%. Then, the form mat is sprinkled with spherical activated carbon based on pitch, and excess activated carbon is removed, and the temperature is increased to 160 °.
At (2 min) the adhesive was allowed to set. The spherical activated carbon has a diameter of 0.4 to 0.6 mm and an inner surface area of 110.
0 m 2 / g and the amount is 195 g / l.
【0032】フイルタ材料を空気チヤンネルに導入した
箇所には、ネジ止め蓋を設けた。側壁、底面および蓋
は、39mmの間隔で、航空機工業で使用される接着剤
(エポキシ樹脂)によつて空気チヤンネルに接着した高
さ約3mmのU字状案内レールを有する。上記案内レー
ルには、298×398×39mmのプレートを正確に
圧入する。A screw-fastening lid was provided at the place where the filter material was introduced into the air channel. The side walls, bottom and lid have U-shaped guide rails with a height of about 3 mm, which are glued to the air channel by means of an adhesive (epoxy resin) used in the aircraft industry, with a spacing of 39 mm. A plate of 298 x 398 x 39 mm is accurately press-fit into the guide rail.
【0033】次いで、装填したフオームから、306×
408×20.5mmの二つのプレートを切り出し、僅
かな圧力によつて案内レールに押込み、蓋を閉鎖した。Then, from the loaded form, 306 ×
Two 408 x 20.5 mm plates were cut out and pushed into the guide rails with slight pressure and the lid was closed.
【0034】他方、比較のため、290×390×2
0.5mmの二つのフオームプレートを合成樹脂フレー
ムに発泡、充填し、上記フレームを空気チヤンネルに導
入した。0.5m/sの窒素中でトルエン1000pp
mを使用して行つた比較測定から、予期に反して、パツ
キンなしで挿入したフイルタは検知可能な縁通過性を示
さないということが判つた。なぜならば、幾分大きく圧
縮し易いフイルタプレートを空気チヤンネルに導入した
ことによつて、縁が完全に密封されるからである。初期
リークは≦1ppmであった。通常のフイルタフレーム
(発泡充填部分も含む)を除去したことによつて、約1
0%大きいフイルタ面積が得られ、従って、最終的に、
フイルタ能力が向上される。On the other hand, for comparison, 290 × 390 × 2
Two 0.5 mm foam plates were foamed and filled in a synthetic resin frame, and the frame was introduced into an air channel. Toluene 1000pp in nitrogen of 0.5m / s
Unexpectedly, comparative measurements made using m revealed that the filter inserted without the packin showed no detectable edge passage. This is because the introduction of a filter plate, which is rather large and easy to compress, into the air channel completely seals the edges. The initial leak was ≦ 1 ppm. By removing the normal filter frame (including the foam filling part), about 1
A filter area of 0% is obtained, and thus finally
The filter ability is improved.
【0035】フイルタ要素の更新は、極めて簡単であ
る。即ち、蓋を開けてフイルタ要素を引出した後、新し
いフイルタプレートを挿入すればよい。Updating the filter elements is quite simple. That is, after opening the lid and pulling out the filter element, a new filter plate may be inserted.
【0036】実施例 2 実施例1と同様に操作した。但し、活性炭球形粒子の代
わりに、炭化、活性化した陽イオン交換樹脂(スルホン
化スチレン・ジビニルベンゼン・コポリマー)を使用し
た。比較測定は実施しなかつた。Example 2 The same operation as in Example 1 was carried out. However, a carbonized and activated cation exchange resin (sulfonated styrene / divinylbenzene copolymer) was used instead of the activated carbon spherical particles. No comparative measurements were made.
【0037】実施例 3 実施例2と同様に操作した。しかしながら、吸着剤とし
て多孔質ポリマー(ダウ・ケミカル社のSorbath
ene)を使用した。吸着剤導入量は、僅か165g/
lに過ぎない。初期リークは、実施例2の場合よりも幾
分大きく、約2ppmである。Example 3 The same operation as in Example 2 was carried out. However, a porous polymer as an adsorbent (Sorbat of Dow Chemical Co.
ene) was used. The amount of adsorbent introduced is only 165 g /
It's just l. The initial leak is about 2 ppm, somewhat higher than in Example 2.
【0038】実施例 4 この場合、疎水性モレキユラーシーブ(デグサ社のDA
Y・Zeolith)からなる大きさ約1mmのプレス
加工材をフイルタマツトに装填した。担体フオームに9
5g/lを装填できた。Example 4 In this case, a hydrophobic molecular sieve (DA from Degussa)
A pressed material having a size of about 1 mm and made of Y. Zeolith) was loaded on the filter tamat. 9 for carrier form
It was possible to load 5 g / l.
【0039】実施例 5 この場合、完全化のため、実施例1の球状活性炭を高価
値のカーボン片(粒径0.5〜0.8mm,内表面積1
650m2 /g)で置換した。被覆量の減少は認められ
ずー球状活性炭の185g/lに比して145g/l
ー、予想通り、縁通過性は認められなかつた。Example 5 In this case, in order to complete the spherical activated carbon of Example 1, high-value carbon pieces (particle size 0.5 to 0.8 mm, inner surface area 1
650 m 2 / g). No decrease in coating amount was observed-145 g / l compared to 185 g / l for spherical activated carbon
-As expected, no edge-passing property was observed.
【0040】実施例 6 実施例5と同様に操作した。しかしながら、双方のフイ
ルタプレートの間に、径1mmの鋼ワイヤからなる粗い
格子(40×40mmの窓)を補強材として導入した。
このような格子は、必要ではないが、気温の高い地域に
おいて特に、有用であることが判明している。補強のた
め、もちろん、別の材料を使用することもできる。更
に、出口以外に補強材を設置することもできる。Example 6 The same operation as in Example 5 was carried out. However, a coarse grid (40 × 40 mm window) made of steel wire with a diameter of 1 mm was introduced as a reinforcement between both filter plates.
Such a grid, although not required, has been found to be particularly useful in hot areas. For reinforcement, of course, other materials can be used. Furthermore, a reinforcing material can be installed in addition to the outlet.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F24F 13/28 (72)発明者 ジョナス・トーンブロム ドイツ連邦共和国デイ−40699 エルクラ ト、アム、デュッセルフェル 42─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location F24F 13/28 (72) Inventor Jonas Tohnblom Federal Republic of Germany Day 40699 Erkrat, Am, Düsselfel 42
Claims (27)
性担体材料からなり僅かに圧縮して空気供給チヤンネル
に導入した自立の弾性吸着フイルタ層の無パツキン・無
フレーム形臭気発生物質および/または有害物質フイル
タとしての使用。1. A non-packing, frameless odor generating substance of a self-supporting elastic adsorption filter layer which is made of a highly permeable carrier material having an adsorbent fixed by an adhesive and is slightly compressed and introduced into an air supply channel, And / or use as a filter for hazardous substances.
または2の使用。3. Claim 1 in a car or means of transportation.
Or use of 2.
網状ポリウレタンフオームからなることを特徴とする請
求項1〜3の一つに記載の使用。4. Use according to one of claims 1 to 3, characterized in that the breathable carrier material consists of reticulated polyurethane foam with large pores.
フオームのスケルトンに固定されていることを特徴とす
る請求項4の使用。5. Use according to claim 4, characterized in that the adsorbent is fixed to the skeleton of the polyurethane foam by means of an adhesive.
iの気孔率を有することを特徴とする請求項4または5
の使用。6. The polyurethane foam is 8 to 30 pp.
6. Porosity of i, 6.
Use of.
タンフオームの気孔径の1/3よりも小さいことを特徴
とする請求項4〜6の一つに記載の使用。7. Use according to one of claims 4 to 6, characterized in that the particle size of the adsorbent is at least smaller than 1/3 of the pore size of the polyurethane foam.
度が、1〜10N/cm3 の圧力において、少なくとも
2%であることを特徴とする請求項4〜7の一つに記載
の使用。8. Use according to one of claims 4 to 7, characterized in that the degree of compression of the charged polyurethane foam is at least 2% at a pressure of 1 to 10 N / cm 3 .
からなることを特徴とする請求項1〜8の一つに記載の
使用。9. Use according to one of claims 1 to 8, characterized in that the adsorption filter layer comprises a multilayer adsorption filter layer.
m(特に、10〜30mm)であることを特徴とする請
求項1〜9の一つに記載の使用。10. The thickness of the adsorption filter layer is 5 to 40 m.
Use according to one of the claims 1 to 9, characterized in that it is m (especially 10 to 30 mm).
する請求項1〜10の使用。11. Use according to claims 1 to 10, characterized in that the adsorbent is activated carbon.
くは、0.3〜1mm)の球形活性炭からなることを特
徴とする請求項1〜11の一つに記載の使用。12. Use according to one of claims 1 to 11, characterized in that the adsorbent consists of spherical activated carbon with a diameter of 0.2 to 2 mm (preferably 0.3 to 1 mm).
/gの内表面積(BET法)を有することを特徴とする
請求項12の使用。13. Spherical activated carbon is at least 900 m 2
Use according to claim 12, characterized in that it has an internal surface area (BET method) of / g.
を使用した場合、少なくとも10N(好ましくは、少な
くとも30N)のバースト圧を有することを特徴とする
請求項12または13の使用。14. Use according to claim 12 or 13, characterized in that the spherical activated carbon has a burst pressure of at least 10 N (preferably at least 30 N) when using balls with a diameter of 0.5 mm.
くは、0.3〜1mm)および内表面積≧900m2 /
gのカーボン片またはカーボン粒からなることを特徴と
する請求項1〜14の一つに記載の使用。15. The adsorbent has a diameter of 0.2 to 2 mm (preferably 0.3 to 1 mm) and an internal surface area ≧ 900 m 2 /
Use according to one of claims 1 to 14, characterized in that it consists of g of carbon flakes or carbon particles.
ニルベンゼン・コポリマーまたはスチレン・アクリル酸
・コポリマーをベースとする炭化、活性化せる多孔質ポ
リマーからなることを特徴とする請求項1〜15の一つ
に記載の使用。16. An adsorbent comprising a carbonized, activatable porous polymer based on a sulfonated styrene-divinylbenzene copolymer or a styrene-acrylic acid copolymer. Use as described in one.
ニルベンゼン・コポリマーまたはスチレン・アクリル酸
・コポリマーをベースとする炭化、活性化せる陽イオン
交換樹脂からなることを特徴とする請求項1〜16の一
つに記載の使用。17. The adsorbent comprises a carbonizing and activating cation exchange resin based on a sulfonated styrene-divinylbenzene copolymer or a styrene-acrylic acid copolymer. Use as described in one.
有するポリスチレン樹脂またはポリアクリル樹脂をベー
スとする炭化、活性化せる陰イオン交換樹脂からなるこ
とを特徴とする請求項1〜17の使用。18. The adsorbent comprises a carbonization-activating anion exchange resin based on a polystyrene resin or a polyacrylic resin having a tertiary or quaternary amino group. use.
橋されたスチレン・ジビニルベンゼン・コポリマーをベ
ースとする多孔質ポリマーからなることを特徴とする請
求項1〜18の一つに記載の使用。19. Use according to one of claims 1 to 18, characterized in that the adsorbent consists of a porous polymer based on a styrene-divinylbenzene copolymer crosslinked via CH 2 bridges. .
成形片からなることを特徴とする請求項1〜19の一つ
に記載の使用。20. Use according to one of claims 1 to 19, characterized in that the adsorbent consists of hydrophobic molecular sieve shaped pieces.
が、50〜400g/l(好ましくは、150〜350
g/l)であることを特徴とする請求項1〜20の一つ
に記載の使用。21. The amount of adsorbent contained in the adsorption filter layer is 50 to 400 g / l (preferably 150 to 350).
Use according to one of the claims 1 to 20, characterized in that it is g / l).
±50%の範囲で対応することを特徴とする請求項1〜
21の一つに記載の使用。22. The amount of adhesive applied corresponds to the weight of the foam within a range of ± 50%.
Use according to one of 21.
(例えば、アクリル酸誘導体、ポリウレタン誘導体、ポ
リスチレン誘導体、ポリシアネート誘導体、ポリビニル
アセテート誘導体または熔融接着剤)を含むことを特徴
とする請求項1〜22の一つに記載の使用。23. The adhesive comprises a crosslinkable organic polymer (eg, acrylic acid derivative, polyurethane derivative, polystyrene derivative, polycyanate derivative, polyvinyl acetate derivative or melt adhesive). Use according to one of 22.
リアミンで架橋されるマスクせるジイソシアナートおよ
び/またはポリイソシアナートをベースとし溶剤を含ま
ないプレポリマー2成分系を含むことを特徴とする請求
項23の使用。24. The adhesive comprises a solvent-free prepolymer two-component system based on masking diisocyanates and / or polyisocyanates which are crosslinked with diamines and / or polyamines. Use of 23.
アナートポリマーおよび/またはポリイソシアネートを
含むことを特徴とする請求項23または24の使用。25. Use according to claim 23 or 24, characterized in that the adhesive comprises unmasked diisocyanate polymers and / or polyisocyanates.
していることを特徴とする請求項1〜25の一つに記載
の使用。26. Use according to one of claims 1 to 25, characterized in that the adsorption filter layer is convexly curved towards the inflow side.
間にまたは空気供給チヤンネルの出口側に設置されてい
ることを特徴とする請求項1〜26の一つに記載の要
素。27. Element according to one of claims 1 to 26, characterized in that a supplementary reinforcing element is provided between the adsorption filter layers or on the outlet side of the air supply channel.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4421217.8 | 1994-06-17 | ||
| DE4421217 | 1994-06-17 | ||
| DE19512028 | 1995-03-31 | ||
| DE19512028.0 | 1995-03-31 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08168633A true JPH08168633A (en) | 1996-07-02 |
Family
ID=25937508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7174368A Pending JPH08168633A (en) | 1994-06-17 | 1995-06-15 | Use of filter for gasket-free/frame-free odor emitting substance and/or harmful substance |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5616169A (en) |
| JP (1) | JPH08168633A (en) |
| DE (1) | DE19521666C2 (en) |
| FR (1) | FR2721232B1 (en) |
| IL (1) | IL114189A (en) |
| IT (1) | IT1276677B1 (en) |
| NL (1) | NL1000567C2 (en) |
| SE (1) | SE509743C2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007169274A (en) * | 2005-12-19 | 2007-07-05 | Bluecher Gmbh | Use of activated carbon and medicinal preparation using activated carbon |
Families Citing this family (41)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE515506C2 (en) * | 1994-06-17 | 2001-08-20 | Mhb Filtration Gmbh & Co Kg | Odor filter for ventilation outlet hoods |
| US5871569A (en) * | 1996-10-15 | 1999-02-16 | Carrier Corporation | Filter material |
| DE19647236C2 (en) * | 1996-11-15 | 2003-06-18 | Draegerwerk Ag | Layered gas filter media, their manufacture and their use |
| DE29700524U1 (en) * | 1997-01-14 | 1997-05-07 | Helsa-Werke Helmut Sandler GmbH & Co. KG, 95482 Gefrees | Device for reducing or eliminating odorants, especially in new vehicles |
| US5989320A (en) * | 1997-05-05 | 1999-11-23 | Rutkowski; Timothy C. | Frameless electrostatic air filter with internal support grill |
| DE19727295A1 (en) * | 1997-06-27 | 1999-01-07 | Bluecher Gmbh | Clean air filter |
| FR2772670B1 (en) * | 1997-12-22 | 2000-02-04 | Valeo | FILTRATION DEVICE FOR FITTING A VENTILATION AND / OR HEATING AND / OR AIR CONDITIONING APPARATUS, PARTICULARLY FOR A VEHICLE |
| JP3912886B2 (en) * | 1998-02-19 | 2007-05-09 | 株式会社ダン・タクマ | Manufacturing method of ion exchange filter |
| CN1160145C (en) * | 1998-08-05 | 2004-08-04 | 东丽株式会社 | Chemical Filtration Units and Gas Purification Systems |
| DE19836469A1 (en) * | 1998-08-12 | 2000-02-17 | Mhb Filtration Gmbh & Co Kg | Air filter for vehicles or buildings has meso and macro pores representing more than half of total for economic manufacture and efficiency with long service life |
| US6447584B1 (en) * | 1998-08-20 | 2002-09-10 | Extraction Systems, Inc. | Filters employing porous strongly acidic polymers |
| DE19845526C5 (en) * | 1998-10-02 | 2016-10-20 | Mann+Hummel Innenraumfilter Gmbh & Co. Kg | Filter material for fluid media and method for producing such a filter material |
| US6346143B1 (en) * | 1999-02-25 | 2002-02-12 | Mcgowan Kimberly F. | Odor adsorptive filter for refrigerators and freezers |
| US6136075A (en) * | 1999-05-03 | 2000-10-24 | Westvaco Corporation | Automotive evaporative emissions canister adsorptive restraint system |
| US6214095B1 (en) * | 1999-07-06 | 2001-04-10 | Donaldson Company, Inc. | Adsorbent pouch for removal of gaseous contaminants |
| DE19931371A1 (en) * | 1999-07-08 | 2001-01-11 | Mhb Filtration Gmbh & Co Kg | Filter material for gas filtration with biocidal properties |
| US20020178706A1 (en) * | 2000-02-04 | 2002-12-05 | The Procter & Gamble Company | Air filtering device |
| US20030019362A1 (en) * | 2000-02-04 | 2003-01-30 | The Procter & Gamble Company | Air deodorization device with a detachable cartridge |
| US7540901B2 (en) * | 2000-05-05 | 2009-06-02 | Entegris, Inc. | Filters employing both acidic polymers and physical-adsorption media |
| JP5595627B2 (en) | 2000-05-05 | 2014-09-24 | インテグリス・インコーポレーテッド | Filters that use both acidic polymers and physisorption media |
| US6762139B2 (en) * | 2001-08-14 | 2004-07-13 | 3M Innovative Properties Company | Flexible adsorbent filter |
| FR2835445B1 (en) * | 2002-02-07 | 2004-11-19 | Air Liquide | USE OF AN ADSORBENT IN THE FORM OF SOLID FOAM FOR THE PURIFICATION OR SEPARATION OF GASES |
| EP1485656A4 (en) * | 2002-02-22 | 2006-05-17 | Kx Industries Lp | Air purifying filter systems for building air supply and respirators useful against nbc attacks |
| US20050211090A1 (en) * | 2003-08-25 | 2005-09-29 | Mccullough Matthew L | Method for achieving ultra-low emission limits in VOC control |
| DE102004022798A1 (en) * | 2004-04-07 | 2005-11-03 | Helsa-Automotive Gmbh & Co. Kg | Filter for use in vehicle that generates hydrocarbon emissions comprises housing that contains filter element comprising adsorption resin particles on support |
| US7597745B2 (en) * | 2004-04-28 | 2009-10-06 | Foamex Innovations Operating Company | Filter materials for adsorbing hydrocarbons |
| US20050241479A1 (en) * | 2004-04-28 | 2005-11-03 | Foamex L.P. | Filter materials for absorbing hydrocarbons |
| US7416581B2 (en) * | 2004-09-03 | 2008-08-26 | Point Source Solutions, Inc. | Air-permeable filtration media, methods of manufacture and methods of use |
| TWI417130B (en) * | 2006-07-13 | 2013-12-01 | Entegris Inc | Filtering system |
| DE102006036355A1 (en) * | 2006-08-02 | 2008-02-07 | Artemis Control Ag | Sorption filter for e.g. process air, comprises stacked, separable individual layers of filter medium containing removable test pieces permitting filtration characteristics to be assessed |
| SE531005C2 (en) * | 2007-03-08 | 2008-11-18 | Envac Ab | Method and system for energy recovery in vacuum-driven waste collection systems |
| DE102007027026A1 (en) * | 2007-06-08 | 2008-12-11 | BLüCHER GMBH | Mat-shaped foam material for air purification and / or air filtration |
| US20100180830A1 (en) * | 2009-01-22 | 2010-07-22 | Fritter Charles F | Animal litter air treatment device containing activated carbon |
| US8621884B2 (en) | 2008-11-12 | 2014-01-07 | Hoffman Enclosures, Inc. | AC unit with economizer and sliding damper assembly |
| DE102008063815A1 (en) * | 2008-12-19 | 2010-06-24 | Hans-Peter Kohlstadt | Open porous molded body based on inorganic light-granules with hydrophobic surface, and organic binders, useful e.g. as furniture panels, preferably for countertops, and as plates for electrical appliances such as refrigerators |
| US8500890B2 (en) * | 2011-03-01 | 2013-08-06 | Faurecia Interior Systems, Inc. | Air channel with integrated odor absorbing element |
| US10960341B2 (en) | 2016-03-14 | 2021-03-30 | 3M Innovative Properties Company | Air filters comprising polymeric sorbents for aldehydes |
| CN108778455B (en) | 2016-03-14 | 2021-12-14 | 3M创新有限公司 | Air filters containing polymeric adsorbents for reactive gases |
| US11305224B2 (en) | 2017-04-18 | 2022-04-19 | 3M Innovative Properties Company | Air filter media with post-pleat-deposited sorbent particles |
| US11278832B2 (en) | 2017-06-16 | 2022-03-22 | 3M Innovative Properties Company | Air filters comprising polymeric sorbents for aldehydes |
| US11285421B2 (en) * | 2018-04-12 | 2022-03-29 | Electrolux Home Products, Inc. | Filter media for filtration of cooking fumes |
Family Cites Families (45)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DD63768A (en) * | ||||
| US2961710A (en) * | 1957-01-04 | 1960-11-29 | Norman H Stark | Method for making a foamed polyurethane filter |
| US4224415A (en) * | 1958-07-18 | 1980-09-23 | Rohm And Haas Company | Polymerization processes and products therefrom |
| US3721072A (en) * | 1970-07-13 | 1973-03-20 | Calgon Corp | Bonded activated carbon air filter |
| US3925248A (en) * | 1971-05-11 | 1975-12-09 | Collo Rheincollodium Koln Gmbh | Filter medium for gases |
| JPS5111085A (en) * | 1974-07-18 | 1976-01-28 | Nippon Kuringeeji Kk | |
| US4040990A (en) * | 1975-02-18 | 1977-08-09 | Rohm And Haas Company | Partially pyrolyzed macroporous polymer particles having multimodal pore distribution with macropores ranging from 50-100,000 angstroms |
| US4013566A (en) * | 1975-04-07 | 1977-03-22 | Adsorbex, Incorporated | Flexible desiccant body |
| JPS5230799A (en) * | 1975-09-04 | 1977-03-08 | Sumitomo Chem Co Ltd | Method for production of porous carbon |
| US4061807A (en) * | 1976-02-09 | 1977-12-06 | Shaler Amos J | Adsorbent body and method for making same |
| JPS565313A (en) * | 1979-06-26 | 1981-01-20 | Kureha Chem Ind Co Ltd | Detoxificating spherical active carbon and preparing the same |
| JPS5489010A (en) * | 1977-12-27 | 1979-07-14 | Kureha Chem Ind Co Ltd | Spherical activated charcoal antidote |
| GB1600374A (en) * | 1978-03-13 | 1981-10-14 | Finch D A | Filter elements and their manufacture |
| JPS5510971A (en) * | 1978-07-12 | 1980-01-25 | Sumitomo Chemical Co | Blood purifying device |
| US4699681A (en) * | 1978-09-08 | 1987-10-13 | D-Mark, Inc. | Method of making a gas phase permeable filter |
| FR2438493A1 (en) * | 1978-10-09 | 1980-05-09 | Takeda Chemical Industries Ltd | FILTER ELEMENT FOR AIR PURIFICATION |
| JPS5584514A (en) * | 1978-12-22 | 1980-06-25 | Hitachi Ltd | Evaporated fuel trap unit |
| JPS5599319A (en) * | 1979-01-23 | 1980-07-29 | Bridgestone Corp | Packed material with activated carbon |
| US4519816A (en) * | 1980-10-01 | 1985-05-28 | The Dow Chemical Company | Method for the recovery of solvent vapors |
| DE3228156C2 (en) * | 1982-07-28 | 1994-01-20 | Bluecher Hubert | Use of a flexible surface filter in an air cleaning device for motor vehicle cabins |
| US4678489A (en) * | 1982-11-19 | 1987-07-07 | John C. Bertelsen | Filtering system for paper handling machines |
| DE3304349C3 (en) * | 1983-02-09 | 1995-10-26 | Bluecher Hubert | Surface filter and process for its manufacture |
| DE8312718U1 (en) * | 1983-04-29 | 1983-09-29 | Sorbexx GmbH Gesellschaft für Adsorptionstechnik und Verbundstoffe, 8586 Gefrees | FILTER INSERT |
| GB8503749D0 (en) * | 1985-02-14 | 1985-03-20 | Craig Med Prod Ltd | Gas filter |
| FR2615099B1 (en) * | 1987-05-14 | 1996-08-23 | Biotrol Sa Lab | FILTER SYSTEM WITH INCORPORATED DEGASSING VENT FOR MOUNTING IN DRAINAGE POCKETS OF ARTIFICIAL ANUSES DURING THEIR MANUFACTURE |
| DE3719419A1 (en) * | 1987-06-11 | 1988-12-29 | Sandler Helmut Helsa Werke | Filter cartridge for a respirator mask |
| DE3719415A1 (en) * | 1987-06-11 | 1988-12-22 | Sandler Helmut Helsa Werke | Filter device and process for the production thereof |
| DE3719418C1 (en) * | 1987-06-11 | 1988-07-21 | Sandler Helmut Helsa Werke | Process for the production of a filter material |
| US4957897A (en) * | 1988-01-29 | 1990-09-18 | Rohm And Haas Company | Carbonaceous adsorbents from pyrolyzed polysulfonated polymers |
| DE3813563C2 (en) * | 1988-04-22 | 2002-01-17 | Mhb Filtration Gmbh & Co Kg | Adsorption filter with high air permeability |
| DE3813564C2 (en) * | 1988-04-22 | 1997-11-06 | Hasso Von Bluecher | Activated carbon filter layer for gas masks |
| DE3817084C1 (en) * | 1988-05-19 | 1989-09-21 | Daimler-Benz Aktiengesellschaft, 7000 Stuttgart, De | Odour-binding filter in the feed air stream of a motor vehicle interior |
| DE3819002A1 (en) * | 1988-06-03 | 1989-12-14 | Hasso Von Bluecher | Air filter for passenger cells |
| US5226937A (en) * | 1989-08-18 | 1993-07-13 | Pall Corporation | Void-containing sorbent pad |
| US5395428A (en) * | 1990-01-23 | 1995-03-07 | Von Bluecher; Hasso | Filter material for motor vehicles |
| DE4027799C2 (en) * | 1990-09-01 | 1995-04-20 | Hasso Von Bluecher | Odor filter for vehicle cabins |
| JPH04197441A (en) * | 1990-11-28 | 1992-07-17 | Osaka Gas Co Ltd | Adsorbent |
| DE4040104A1 (en) * | 1990-12-16 | 1992-06-17 | Behr Gmbh & Co | FILTERS FOR AN AIR CONDITIONING OR HEATING SYSTEM FOR A MOTOR VEHICLE |
| DE9108353U1 (en) * | 1991-07-06 | 1992-10-29 | Helsa-Werke Helmut Sandler GmbH & Co KG, 8586 Gefrees | Filter, especially for a vehicle |
| DE4304026B4 (en) * | 1992-02-28 | 2005-02-17 | Mhb Filtration Gmbh & Co. Kg | Process for disposal of spent ion exchangers |
| US5266090A (en) * | 1992-09-21 | 1993-11-30 | Dust Free, Inc. | Multi-sided air filter with wraparound filter media |
| DE4241605A1 (en) * | 1992-12-10 | 1994-06-16 | Hasso Von Bluecher | High air permeability filter system - has coarsely porous absorption section followed by finely porous absorption section. |
| US5350444A (en) * | 1993-01-25 | 1994-09-27 | The Healthwise Auto Filter Inc. | Passenger vehicle with a filtered air intake |
| US5350443B2 (en) * | 1993-04-19 | 1999-08-10 | Von Hasso Bluecher | Filter sheet material for passenger cabins in motor vehicles |
| DE4328219A1 (en) * | 1993-08-21 | 1995-02-23 | Hasso Von Bluecher | Spheres of activated carbon from ion exchangers |
-
1995
- 1995-06-07 SE SE9502085A patent/SE509743C2/en not_active IP Right Cessation
- 1995-06-08 IT IT95MI001205A patent/IT1276677B1/en active IP Right Grant
- 1995-06-14 DE DE19521666A patent/DE19521666C2/en not_active Expired - Lifetime
- 1995-06-15 JP JP7174368A patent/JPH08168633A/en active Pending
- 1995-06-16 FR FR9507235A patent/FR2721232B1/en not_active Expired - Lifetime
- 1995-06-16 IL IL114189A patent/IL114189A/en not_active IP Right Cessation
- 1995-06-16 NL NL1000567A patent/NL1000567C2/en not_active IP Right Cessation
- 1995-06-19 US US08/491,631 patent/US5616169A/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007169274A (en) * | 2005-12-19 | 2007-07-05 | Bluecher Gmbh | Use of activated carbon and medicinal preparation using activated carbon |
Also Published As
| Publication number | Publication date |
|---|---|
| NL1000567A1 (en) | 1995-12-18 |
| IL114189A (en) | 1998-02-22 |
| DE19521666C2 (en) | 2002-02-14 |
| DE19521666A1 (en) | 1996-01-11 |
| NL1000567C2 (en) | 1997-07-09 |
| ITMI951205A1 (en) | 1996-12-08 |
| FR2721232B1 (en) | 1998-10-02 |
| SE9502085L (en) | 1995-12-18 |
| ITMI951205A0 (en) | 1995-06-08 |
| IT1276677B1 (en) | 1997-11-03 |
| IL114189A0 (en) | 1995-10-31 |
| FR2721232A1 (en) | 1995-12-22 |
| US5616169A (en) | 1997-04-01 |
| SE509743C2 (en) | 1999-03-01 |
| SE9502085D0 (en) | 1995-06-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH08168633A (en) | Use of filter for gasket-free/frame-free odor emitting substance and/or harmful substance | |
| US5807424A (en) | Regenerative adsorption filter bed for exhauster hoods | |
| US20190001253A1 (en) | Filter medium | |
| US4800190A (en) | Filter material and process for the production thereof | |
| EP1508359B1 (en) | Dehumidification system and dehumidification method | |
| EP1406716B1 (en) | Filter element | |
| JP5048454B2 (en) | Adsorption / desorption element, carbon dioxide concentration adjusting device using the same, carbon dioxide concentration adjusting system, and carbon dioxide concentration adjusting method. | |
| US5332426A (en) | Agglomerated activated carbon air filter | |
| US4296166A (en) | Air filter of polyurethane mesh containing carbon adsorbent | |
| US11369914B2 (en) | Process and apparatus for the removal of metabolic carbon dioxide from a confined space | |
| EP0803275A1 (en) | Air filter | |
| GB2163064A (en) | Self-supporting absorbent structure | |
| US20100162888A1 (en) | Mat-shaped foam material for cleaning and/or filtering air | |
| US11878266B2 (en) | Regenerable air filter | |
| JPH05305213A (en) | Air purifying sheet and air purifying filter using the same | |
| US6197079B1 (en) | Pleated air filter and method for producing same | |
| US7759275B2 (en) | Sorbent system for water removal from air | |
| US6551700B2 (en) | Spherical high-performance adsorbents with microstructure | |
| WO1994003270A1 (en) | Agglomerated activated carbon air filter | |
| US20240198262A1 (en) | Air Filter Medium, Filter Medium Body, and Filter Element | |
| CA2049978A1 (en) | Filter material for motor vehicles | |
| JPH1043530A (en) | Air purifying filter | |
| KR20080093699A (en) | Manufacturing method of laminated composite adsorption material | |
| KR20230062025A (en) | Composite-type multi-layered Chemical Filter and preparation method thereof | |
| KR100647344B1 (en) | Manufacturing method of chemical adsorption filter for air purification |